The present invention relates to poly(ester-ether) compositions and to a process for their preparation. In particular, the invention relates to poly(ester-ether) compositions obtained by reacting a polyester which is prepared from a dicarboxylic acid and an aliphatic diol with a dihydroxy aromatic compound in the presence of a metal catalyst. Incorporation of the dihydroxy aromatic compound into the polyester chain causes an increase in the Tg value and increases the thermal stability of the polyester. These poly(ester-ether) compositions are useful in molded articles of all types.

Description

34 parts

›FIELD OF THE INVENTION

›BACKGROUND OF THE INVENTION

When a polyester is treated at elevated temperatures with a diol, the expected reaction is a transesterification reaction in which diol moieties of the polyester chain are liberated and new diol moieties are inserted into the polyester chain. In contrast, the present inventors have unexpectedly discovered that where the diol reactant is different from that of the diol moieties in the starting polyesters, copolymers are obtained. More specifically, the present inventors have determined that dihydroxy aromatic compounds inserted into the chain of a polyester which is prepared from a dicarboxylic acid and an aliphatic diol, have predominantly ether linkage rather than ester linkages. Thus, poly(ethylene terephthalate) treated with hydroquinone, for example, has mono- and diether linkages. Incorporation of the dihydroxy aromatic compounds into the polyester chain causes an increase in the glass transition temperature (Tg) value and the thermal stability of the polyester. For example, the Tg value of poly(ethylene terephthalate) has been increased from 72° C. to 100° C. by modification with certain dihydroxy aromatic compounds.

›SUMMARY OF THE INVENTION

Accordingly, it is one object of the present invention to provide poly(ester-ether) compositions. Accordingly, it is another object of the invention to provide a process for preparing poly(ester-ether) compositions which are useful in applications requiring thermal stability.

These and other objects are accomplished herein by a poly(ester-ether) composition having improved thermal stability comprising repeat units from the reaction of

(1) 10 to 175 mole percent based on the repeat units of the polyester, component (2), of at least one dihydroxy aromatic compound, with

(2) a polyester consisting essentially of repeat units from:

(a) at least one dicarboxylic acid; and

(b) at least one diol selected from the group consisting of aliphatic and cycloaliphatic diols, provided that at least 50 mole percent of the diol is an aliphatic diol having 2 to 20 carbon atoms, based on 100 mole percent dicarboxylic acid and 100 mole percent diol.

The present invention also relates to a process for preparing a poly(ester-ether) having improved thermal stability comprising

(I) reacting

(1) 10 to 175 mole percent based on the repeat units of the polyester, component (2), of at least one dihydroxy aromatic compound, with

(2) a polyester consisting essentially of repeat units from:

(a) at least one dicarboxylic acid; and

(II) forming the poly(ester-ether) into a molded or extruded article.

›DESCRIPTION OF THE INVENTION · 1 of 2

The present invention relates to poly(ester-ether) compositions which contain repeat units from the reaction of a dihydroxy aromatic compound, component (1), with a polyester, component (2). Dihydroxy aromatic compounds suitable for use as component (1) include: hydroquinone, resorcinol, catechol, 4,4'-biphenol, bisphenol A, phenylhydroquinone, methylhydroquinone, 1,4-dihydroxynaphthalene, and chlorohydroquinone. From to 175 mole percent, based on the repeat units of the polyester, of the dihydroxy aromatic compound is reacted with the polyester. Preferably, the dihydroxy aromatic compound is used in an amount of 20 to 60 mole percent, more preferably 30 to 40 mole percent, based on the repeat units of the polyester. Using less than 10 mole percent of the dihydroxy aromatic compound does not have a significant effect on increasing the Tg of the polymer. Using greater than 175 mole percent of the dihydroxy aromatic compound results in unacceptable levels of branching and a brittle polymer.

Polyesters, component (2), which are useful in the present invention contain repeat units from at least one dicarboxylic acid and at least one aliphatic or a combination of aliphatic and cycloaliphatic diols. The dicarboxylic acid, component (a), is selected from aliphatic dicarboxylic acids preferably having 4 to 14 carbon atoms, cycloaliphatic dicarboxylic acids preferably having 8 to 12 carbon atoms, and aromatic dicarboxylic acids preferably having 8 to 14 carbon atoms. Examples of these dicarboxylic acids include 2,6-, 1,5-, 1,8- or 2,7-naphthalene dicarboxylic acid, succinic, dodecanedioic, glutaric, adipic, trimethyladipic, pimelic, 2,2-dimethylglutaric, azelaic, sebacic, fumaric, suberic, 1,3-cyclopentane dicarboxylic, 1,2-cyclohexanedicarboxylic, 1,3-cyclohexanedicarboxylic, 1,4-cyclohexanedicarboxylic, phthalic, terephthalic, isophthalic, 2,5-norbornanedicarboxylic, diphenic, 4,4'-oxydibenzoic, diglycolic, thiodipropionic, and 4,4'-sulfonyldibenzoic. The anhydride, acid chloride, and ester derivatives of the above acids may also be used. The preferred dicarboxylic acid(s) are isophthalic acid and terephthalic acid.

The diol component, component (b), of the polyester consists of at least 50 mole percent of an aliphatic diol having 2 to 20 carbon atoms, based on 100 mole percent dicarboxylic acid and 100 mole percent diol. In addition to the aliphatic diol, a cycloaliphatic diol may also be present in an amount up to 50 mole percent. The cycloaliphatic diol preferably has 6 to 20 carbon atoms. Included within the class of aliphatic diols are aliphatic diols having ether linkages such as polydiols having 4 to 800 carbon atoms. Suitable aliphatic diols include: ethylene glycol, diethylene glycol, triethylene glycol, 1,2-propanediol, 1,3-propanediol, 2,4-dimethyl-2-ethylhexane-1,3-diol, 2,2-dimethyl-1,3-propanediol, 2-ethyl-2-butyl-1,3-propanediol, 2-ethyl-2-isobutyl-1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, and 2,2,4-trimethyl-1,6-hexanediol. Suitable cycloaliphatic diols to be used with the aliphatic diol(s) include: 1,2-cyclohexanedimethanol, 1,3-cyclohexanedimethanol, and 1,4-cyclohexanedimethanol.

Semi-crystalline and amorphous materials are within the scope of the present invention. In addition, scrap or recycled poly(ethylene terephthalate) may also be used. It is to be understood that the polyesters of this invention contain substantially equal molar proportions of acid equivalents (100 mole %) to hydroxy equivalents (100 mole %). Thus, the polyester comprised of components (a) and (b) will have a total of acid and hydroxyl equivalents equal to 200 mole percent. The polyesters have an inherent viscosity of up to 1.0 dl/g, preferably 0.2 to 0.6 dl/g.

The polyester, component (2) can be prepared by conventional polycondensation procedures well-known in the art. Such processes include direct condensation of the dicarboxylic acid(s) with the diol(s) or by ester interchange using lower alkyl esters. For example, a typical procedure consists of two stages. The first stage, known as ester-interchange or esterification, is conducted in an inert atmosphere at a temperature of 175° C. to 240° C. for 0.5 to 8 hours, preferably 1 to 4 hours. The diols, depending on their particular reactivities and the specific experimental conditions employed, are commonly used in molar excesses of 1.05 to 2.5 per mole of total dicarboxylic acid.

The second stage, referred to as polycondensation, is conducted under reduced pressure at a temperature of 230° C. to 350° C., preferably 265° C. to 325° C., and more preferably 270° C. to 290° C. for 0.1 to 6 hours, preferably 0.25 to 2 hours. Because high melt viscosities are encountered in the polycondensation stage, it is sometimes advantageous to employ temperatures above 300° C. since the resulting decrease in melt viscosity allows somewhat higher molecular weights to be obtained. Stirring or appropriate conditions are employed in both stages to ensure sufficient heat transfer and surface renewal for the reaction mixture. The reactions of both stages are facilitated by appropriate catalysts which are well known in the art. Suitable catalysts include, but are not limited to, alkoxy titanium compounds, alkali metal hydroxides and alcoholates, salts of organic carboxylic acids, alkyl tin compounds and metal oxides.

The poly(ester-ether) compositions are prepared by heating the polyester, component (2), with up to 175 mole percent, based on the repeat unit of the polyester, of the dihydroxy aromatic compound, component (1), in the absence of air for a sufficient time to cause a reaction between the dihydroxy aromatic compound and the polyester. Reaction time for the poly(ester-ether) and dihydroxy aromatic compound are generally in the range of 1 hour to 12 hours at temperatures of 200° C. to 290° C. depending on the polyester being used. Vacuum is then applied for 30 minutes to 5 hours at a temperature of 270° C. to 300° C. to build up the molecular weight of the poly(ester-ether). The polyester, component (2), does not have to be completely molten, especially during the early part of the reaction. The poly(ester-ether) is extruded into strands and pelletized.

›DESCRIPTION OF THE INVENTION · 2 of 2

Optionally, a metal catalyst, component (3), is added to the ether forming reaction. The metal catalyst is preferably present in an amount of 50 ppm catalyst (metal) to 600 ppm catalyst (metal). The catalyst may be one or more of the ester exchange and/or polycondensation catalysts known in the art. Preferably, the catalyst is titanium or tin derived from tetraisopropyl titanate or stannous oxalate. In many cases, it is advantageous to add a co-catalyst, such as a potassium salt, e.g. potassium carbonate, along with the titanium and tin catalysts, to obtain reduced color in the poly(ester-ether) product. It has also been found that zeolite molecular sieves, such as zeolite 4A, can be used as the catalyst. The color of the product increases appreciably as the catalyst metals content increases, and the poly(ester-ether) products may become appreciably branched at the higher catalyst metals contents.

For those poly(ester-ether) products which have sufficient crystallinity, the molecular weight of the poly(ester-ether) may be increased by solid state polymerization. For example, poly(ester-ether) powders, granules, or pellets may be heated under vacuum or heated while passing an inert gas through the reaction vessel to remove liberated condensation by-products. Solid state polymerization is generally conducted for 1 to 24 hours to provide high molecular weight polymers with inherent viscosities of 0.7 to 1.2.

Additives such as fillers, stabilizers, antioxidants, buffers, colorants, dyes, pigments and the like normally used with polymers may be used if desired. Such additives, their amounts, and their use are well known in the art.

The poly(ester-ether) products of this invention are readily melt processed into useful shapes and forms. For example, they may be melt pressed or extruded into films, extruded into rods or other shapes, injection molded or compression molded into various objects, and injection molded preforms may be reheated and blown into bottles, jars and the like.

The materials and testing procedures used for the results shown herein are as follows:

Inherent viscosity (I.V.) was measured at 25° C. using 0.50 grams of polymer per 100 ml of a solvent consisting of 60% by weight phenol and 40% by weight tetrachloroethane. The polymer samples were dissolved without heat.

Ti catalyst source was titanium tetraisopropoxide in n-butanol.

Sn catalyst source was n-butylstannoic acid or stannous oxalate as noted.

Film Strength. Films of vacuum-dried polymer were pressed at 270° C. for 15-20 sec. on a Hannafin press at the final vacuum build up temperature, quenched in cold water and the film strength was assessed by hand creasing.

Mole % Bisphenol A was determined by H Nmr in trifluoracetic acid. The mole % Bisphenol A was calculated as the total Bisphenol A species divided by the total Bisphenol A species plus the total ethylene glycol-derived species multiplied by 100.

Mole % hydroquinone (HQ) was determined by H Nmr in trifluoracetic acid and CDCl 3 . Mole % HQ is calculated as the total amount of hydroquinone (--O--PH--O--) species (whether present as ester, monoethyl ether, or bisethyl ether of hydroquinone) divided by the sum of the total of the hydroquinone species plus the calculated amount of ethylene glycol-derived species (ester+ethers) multiplied by 100. The amount of diethylene glycol species is excluded from the ethylene glycol-derived species.

Mole % of ester/mono/bis(ethyl ether) of hydroquinone was determined by H Nmr in trifluoracetic acid and CDCl 3 .

Mz/Mn was determined as PET equivalents by mixed column Gel Permeation Chromatography (GPC) in 70/30 CH 2 Cl 2/ HFIP.

Glass transition temperature (Tg) was determined using a differential scanning calorimeter (DSC).

Melting point (Tm) was determined using a differential scanning calorimeter (DSC).

The composition and process of the present invention will be further illustrated by a consideration of the following examples, which are intended to be exemplary of the invention. All parts and percentages in the examples are on a weight basis unless otherwise stated.

›Examples3

›EXAMPLE 1

Reaction of HQ and PET without additional catalyst.

Polyethylene terephthalate was prepared using dimethyl terephthalate and ethylene glycol. The catalyst system contained 75 ppm of manganese, 225 ppm of antimony, 80 ppm of cobalt, 20 ppm of titanium and 125 ppm of phosphorous. The PET had a I.V. of 0.61 dL/g.

The polyethylene terephthalate, prepared above, 38.4 grams (0.2 moles) and 8.8 grams (0.08 moles) of hydroquinone were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The flask was evacuated and flushed with nitrogen three times. The flask was partially immersed in a Belmont metal bath at 120° C. The metal bath temperature was immediately increased to 270° C. which took 15-20 minutes to attain. Stirring was begun as soon as the starting materials partially melted. The reaction mixture was stirred under nitrogen for 120 minutes at 270° C., then for 60 minutes at 290° C. Vacuum was applied for 10-15 minutes, and the molecular weight of the polymer was built up under high vacuum (<0.5 torr) as indicated in the table. The polymer was allowed to cool to room temperature under a nitrogen atmosphere.

The polymer had an I.V. of 0.42, a melting point of 208° C., and a Tg of 78° C. Proton NMR analysis indicated that the polymer contained 17 mole % hydroquinone moieties (21 mole % was present as the ester, 63 mole % was present as the monoether and 16 mole % was present as the diether). Additional test results are summarized in Table I.

›EXAMPLE 2 · 1 of 2

Reaction of HQ with bis(2-hydroxyethyl)terephthalate.

Bis(2-hydroxyethyl)terephthalate, 50.8 grams, (0.2 moles), 8.8 grams (0.08 moles) of hydroquinone and 0.11 grams of stannous oxalate (150 ppm Sn based on polymer weight) were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The polymer was prepared using the procedure set forth in Example 1. Reaction times and temperatures are listed in Table I. The yield of polymer was 40.73 grams (96% yield).

The polymer had an I.V. of 0.63, a melting point of 211° C. (ΔHf=2.4 cal/g), and a PET equivalent molecular weight (determined by GPC analysis in methylene chloride/hexafluoroispropanol mixed solvent) as follows: Mn 18,564; Mw 68,899; Mz 260,930; Mw/Mn 3.71; Mz/Mn 14.05. Proton NMR analysis indicated that the polymer contained 12.7 mole % hydroquinone and 5.68 mole % diethylene glycol. Of the hydroquinone present in the polymer, 0.67 mole % was present as the ester, 43.6 mole % was present as the monoether and 55.7 mole % was present as the diether. Additional test results are summarized in Table I.

EXAMPLES 3-11

Reaction of PET With Hydroquinone

The reactions were conducted using the procedure set forth in Example 1. Reaction times and temperatures are listed in Table I. The test results are summarized in Table I.

The results in Table I clearly shows that the Tg of PET is significantly increased from 78 to 104° C. by reacting the PET with a dihydroxy aromatic compound. In addition, the results show that a low molecular weight polyester of bis(2-hydroxyethyl)terephthalate can be significantly increased by reacting the polyester with with a dihydroxy aromatic compound. It is important to note that Example 10 sets forth the upper limit of 175 mole percent. Example 11 which is above 175 mole percent forms a brittle film.

EXAMPLES 12-18

Reaction of PET With Bisphenol A.

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of bisphenol A as listed in Table II, and Sn from n-butylstannoic acid, or Ti from titanium tetraisopropoxide in n-butanol solution, or a mixture of the Sn/Ti were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table II along with the test results.

The results in Table II clearly show that PET modified with the dihydroxy aromatic compounds achieve high inherent viscosities. In addition, the results show that hexafluorobisphenol A does not work as a dihydroxy aromatic compound.

EXAMPLES 19-22

Reaction of PET With 4,4'-Biphenol

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of 4,4'-Biphenol as listed in Table III, and Sn from n-butylstannoic acid, and/or Ti from titanium tetraisopropoxide in n-butanol solution, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table III along with the test results.

The results in Table III clearly show that the Tg of PET is significantly increased by reacting the PET with a dihydroxy aromatic compound. In addition, the results show that high levels of branching (large Mz/Mn) may lead to brittle films as determined by Example 21.

EXAMPLES 23-43

Reaction of PET with Hydroquinone in the presence of Potassium Carbonate

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of hydroquinone as listed in Table IV, Ti from titanium tetraisopropoxide in n-butanol solution, and potassium carbonate, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table IV along with the test results.

The results in Table IV clearly show that potassium carbonate improves the color of the polymers.

EXAMPLES 44-57

Thermal Stability of PET Polymers Modified With Hydroquinone

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of hydroquinone as listed in Table V, and the catalysts as indicated in Table V, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. A sample of PET without any aromatic diol was used as a comparison example. The polymers were evaluated for thermal stability by thermal gravimetric analysis. The test results are summarized in Table V.

The results in Table V clearly show that PET reacted with a dihydroxy aromatic compound are much more stable than the control PET sample.

EXAMPLES 58-64

Reaction of PET with Hydroquinone in the presence of Zeolite 4A Molecular Sieve Catalyst

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of hydroquinone as listed in Table VI, and the indicated amount of Zeolite 4A molecular sieve powder as catalyst/promoter, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table VI along with the test results.

The results in Table VI clearly show that zeolites can be used as catalysts in amounts of 0.1 to less than 5.0 weight percent. Moreover, 1.0 weight percent is the preferred amount.

EXAMPLES 65-75

Reaction of PET With Hydroquinone and Ethylene Glycol.

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of hydroquinone as listed in Table VII, the indicated amount of ethylene glycol, and Sn from stannous oxalate, and/or Ti from titanium tetraisopropoxide in n-butanol solution, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table VII along with the test results.

›EXAMPLE 2 · 2 of 2

The results in Table VII clearly show that the Tg of PET can be significantly increased by reacting PET with a dihydroxy aromatic compound and ethylene glycol.

EXAMPLES 75-78

Reaction of PET With Phenylhydroquinone

The polyethylene terephthalate, prepared in Example 1, 38.4 grams (0.2 moles), the mole percent of phenylhydroquinone as listed in Table VIII, and Sn from stannous oxalate, and/or Ti from titanium tetraisopropoxide in n-butanol solution, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table VIII along with the test results.

The results in Table VIII indicate that certain dihydroxy aromatic compounds such as phenylhydroquinone require larger amounts of catalyst to react with PET probably because of steric hinderance.

EXAMPLES 79-82

Reaction of Selected Terephthalate Homo- and Copolyesters with Hydroquinone

Polymer A or Polymer B, 54.8 grams (0.2 moles), the mole percent of hydroquinone as listed in Table IX, and Sn from stannous oxalate, and/or Ti from titanium tetraisopropoxide in n-butanol solution, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table IX along with the test results.

The results in Table IX clearly shows that the polyesters based on 1,4-cyclohexanedimethanol were not as reactive as the polyesters prepared from PET. In addition, the PET copolyester containing 33 mole % 1,4-cyclohexanedimethanol was much more reactive than those polymers based on 100 mole % 1,4-cyclohexanedimethanol.

EXAMPLES 83-88

Reaction of Various Polyesters With Aromatic Diols.

Polymers D, F, G, H, and I, 0.2 moles, the mole percent of hydroquinone (HQ), or bisphenol A (BPA), as listed in Table X, and Sn from stannous oxalate, and/or Ti from titanium tetraisopropoxide in n-butanol solution, were placed into a glass flask equipped with a metal stirrer and provisions for applying vacuum and maintaining a nitrogen atmosphere. The reactions were conducted using the procedure set forth in Example 1. Specific reaction times and temperatures are listed in Table X along with the test results.

__________________________________________________________________________

›PET MODIFIED WITH HYDROQUINONE

Additional

Stage I

Stage II

Vacuum

Catalyst

Heat Heat Buildup H Nmr

Mono/Bis

HQ Sn/Ti,

Time Time Temp/Time

I.V.

Film HQ Ether of HQ

Mz/ Tg Tm

mole %

ppm °C./Hr.

°C./Hr.

dL/g

Strength

mole %

%/%/% Mn °C.

°C.

__________________________________________________________________________

40 None 270/2.0

290/1.0

290/4.5

0.42

creasable

17.7 21/63/16

9.1 78 208

40(a)

150/0 230/4/0

250-270/2

290/2.25

0.63

tough

12.7 0.7/43.6/55.7

14.1

-- 211

40 100/50

270/2.0

320/1.0

320/0.7

0.78(d)

tough

27.7 19/59/22

15.9

84 228

40 600/0 270/1.0

290/1.0

290/1.7

0.64

v. tough

19.9 22/63/15

11.3

80 None

40 400 ppm

270/1.0

290/1.0

290/3.1

0.56

tough

18.1 23/65/12

4.3 81 None

Sb(b)

90 0/150 270/1.0

290/1.0

1.02

v. tough

39.5 19/68/13

16.1

87 None

125 None 270/2.0

290/1.0

290/3.6

0.31

brittle

56.2 18/67/15

2.4 84 None

125 0/50 270/1.0

290/1.0

290/3.0

0.76

v. tough

53.1 19/69/12

15.6

90 None

175 0/50 270/1.0

290/1.0

290/2.5

0.75

v. tough

64.7 17/73/10

17.1

90 None

175 150/0(c)

270/1.0

290/1.0

290/3.0

0.87

v. tough

-- -- 2.4 -- 219

200 0/50 270/1.0

290/1.0

290/3.3

0.1(d)

brittle

-- -- 2.07

104

None

(e)

__________________________________________________________________________

(a) PET monomer [bis(2hydroxyehtyl terephthalate)] was used instead of PE

polymer.

(b) Catalyst, in this case, was antimony III ethylene glycoxide.

(d) Insoluble material noted in the I.V. solvent.

(e) On first heating cycle, endotherms were detected at 158° C. an

179° C. (1.1 and 0.5 cal/g, respectively).

__________________________________________________________________________

›PET MODIFIED WITH BISPHENOL A

Additional Vacuum H Nmr

Bisphenol

Catalyst

Heat Heat Heat Buildup Bis

A Sn/Ti,

Time Time Time Temp/Time

I.V.

Film phenol A Tg Tm

mole % ppm °C./Hr.

°C./Hr.

dL/g

Strength

mole %

Mz/Mn

°C.

__________________________________________________________________________

20 100/50

None 1 1 270/1.9

0.45

tough

7.6 -- 82 229

20(a) 100/50

None 1 1 270/2.0

0.35

tough

-- 2.5 87 240

30 100/50

None 1.3 1 270/2.0

0.39

tough

9.5 3.2 82 223

30 100/50

230/2.0

1 None 290/2.5

0.65

v. tough

10.9 7.3 84 None

30 0/150 230/2.0

1 1 290/1.5

0.77

v. tough

14.0 19.3 86 None

50 100/0(c)

230/2.0

1 1 290/4.0

0.42

tough

14.2 2.8 86 None

30(b) 150/0(c)

230/4.0

1 1 290/30 0.31

brittle

14.2 4.0 87 None

__________________________________________________________________________

(a) In this case, the PET used was terephthalic acidbased prepared with

the following catalyst: Co = 69; Sb = 184; P = 91.

(b) Hexafluorobisphenol A or(4,4'-hexafluoroisopropylidenediphenol).

__________________________________________________________________________

PET MODIFIED WITH 4,4'-BIPHENOL

Additional Vacuum H Nmr

4,4'-

Catalyst

Heat Heat Buildup 4,4'-

Biphenol

Sn/Ti,

Time Time Temp/Time

I.V.

Film Biphenol Tg Tm

mole %

ppm °C./Hr.

°C./Hr.

dL/g

Strength

mole %

Mz/Mn

°C.

__________________________________________________________________________

25 100/50

270/1.0

290/1.1

290/2.0

0.55

tough

13.6 7.7 90 227

35 100/50

270/1.0

290/1.1

290/2.0

0.47

tough

18.3 5.3 86 216

45 100/50

270/2.0

320/1.1

320/0.3

0.68

brittle(a)

36.4 15.7 92 197

65 100/50

270/1.0

290/1.0

290/1.5

0.45

tough

34.5 5.9 88 199

__________________________________________________________________________

(a) The brittleness is probably the result of excess branching as

determined by the large Mz/Mn value.

__________________________________________________________________________

PET MODIFIED WITH HYDROQUINONE: Effect of Potassium (Carbonate) as a

Cocatalyst with Titanium

(Polymerizations at 270° C./1 Hr. + 290° C./1 Hr. +

290° C./Vacuum/0.7-2.0 Hr.)

Ester/

Starting

Catalyst Pressed

H Nmr

Mono-Bis-

Materials

Ti/K I.V.

Film Film HQ Ether of HQ Tg Tm

(a) ppm dL/g

Strength

Color Mole %

%/%/% Mz/Mn

°C.

__________________________________________________________________________

PET + 40 HQ

50/0 0.60

very tough

amber 17.5 23/64/13

3.2 81 None

PET + 40 HQ

50/50

0.53

very tough

med-lt amber

18.2 21/64/15

5 83 None

PET + 40 HQ

50/100

0.56

very tough

lt. amber

17.6 21/66/13

5 84 None

PET + 40 HQ

50/150

0.58

very tough

lt. yell-amber

17.3 23/65/12

4.6 84 None

PET + 40 HQ

50/200

0.60

very tough

lt. yell-amber

15.5 23/66/12

5.3 85 None

PET + 40 HQ

50/400

0.54

very tough

lt. amber

17.2 21/67/12

7.4 85 198

PET + 40 HQ

100/100

0.54

very tough

lt. yell-amber

16.6 22/64/14

4.3 84 None

PET + 40 HQ

100/150

0.76

very tough

lt. amber

17.4 20/66/14

16.6 85 187

PET + 40 HQ

100/200

0.60

very tough

lt. amber

17.7 20/66/14

9.9 84 208

PET + 40 HQ

150/0

0.98

very tough

dk. red-amber

16.6 20/66/14

14.0 84 None

PET + 40 HQ

150/100

0.60

very tough

med amber

15.6 21/67/12

7.8 81 216

PET + 40 HQ

150/200

0.68

very tough

med amber

16.7 21/63/16

8.4 79 None

PET + 90 HQ

50/0 0.67

very tough

dk. amber

39.4 19/68/13

15.6 87 None

PET + 90 HQ

50/50

0.53

very tough

med. amber

37.0 17/70/13

5.2 86 None

PET + 90 HQ

50/100

0.73

very tough

med-lt. amber

38.2 18/70/12

11.6 90 None

PET + 90 HQ

50/150

0.48

tough (thin)

lt. amber

37.3 17/70/13

4.3 86 None

PET + 125 HQ

50/0 0.76

very tough

med. amber

53.1 19/69/12

15.6 90 None

PET + 125 HQ

50/100

0.59

very tough

amber 50.4 16/71/13

6.8 89 None

PET + 125 HQ

50/150

0.26

brittle

amber 50.1 16/68/14

2.3 82 None

PET + 125 HQ

50/200

0.36

brittle

-- 47.1 16/70/14

2.8 85 None

PET + 125 HQ

100/300

0.36

brittle

med. amber

45.5 16/71/13

2.8 84 None

__________________________________________________________________________

Thermal Stability of PET + Hydroquinone Polymers by Scanning

Thermogravimetric Analysis

Catalysts, ppm

Polymer Used in Rxn of

Initial Wt.

TGA (a) (Heating Rate = 20° C./Min in

N.sub.2)

Ex. Composition

PET With HQ

Loss ˜°C.

˜1 wt. % °C.

˜2 wt. % °C.

˜5 wt. %

˜10 wt. %

°C.

__________________________________________________________________________

Control

PET Mn/Sb/Co/Ti/P

330 375 385 400 411

44 PET + 40% HQ

50 Ti 385 405 410 425 437

45 PET + 40% HQ

100 Ti 380 400 410 420 431

46 PET + 40% HQ

150 Ti 385 405 415 430 440

47 PET + 40% HQ

50 Ti/100 K

-- -- -- -- 448

48 PET + 40% HQ

50 Ti/150 K

-- -- -- -- 438

49 PET + 40% HQ

50 Ti/200 K

-- -- -- -- 438

50 PET + 40% HQ

100 Ti/150 K

-- -- -- -- 430

51 PET + 40% HQ

100 Ti/200 K

-- -- -- -- 449

52 PET + 40% HQ

100 Ti/400 K

-- -- -- -- 433

53 PET + 40% HQ

50 Ti(d) -- -- -- -- 453

54 PET + 40% HQ

150 Ti/200 K

385 400 405 420 429

55 PET + 40% HQ

300 Sn(b)

385 405 410 420 437

56 PET + 40% HQ

300 Sn(c)

385 400 405 420 431

57 PET + 125% HQ

50 Ti/200 K

-- -- -- -- 436

__________________________________________________________________________

(a) Thermogravimetric Analyses (TGA) weight loss data at other than 10

weight percent loss are estimates from TGA curves.

(b) Source of Sn was nbutylstannoic acid.

(d) The heating schedule for this sample was 250° C. for 2 hours

plus 270° C. for 1 hour plus 290° C. with vacuum.

__________________________________________________________________________

PET MODIFIED WITH HYDROQUINONE: Effect of Zeolite 4A as a Catalyst

Catalyst Vacuum H Nmr

Ester/

Zeolite

Heat Heat Buildup 4,4-bi

Mono/Bis

Starting

4A Time Time Temp/Time

I.V.

Film (a)

phenol

Ether of HQ Tg Tm

Materials

Wt % °C./Hr.

°C./Hr.

dL/g

Strength

Mole %

%/%/%/ Mz/Mn

°C.

__________________________________________________________________________

›PET +

None 270/2.0

290/1.0

290/4.5

0.42

creasable

17.7 21/63/16

9.1 78 208

40% HQ

›PET +

None -- 290/3.0

290/3.0

0.34(c)

tough (-)

22.7 17/63/20

2.4 82 None

40% HQ

›PET +

0.10 270/2.0

290/1.0

290/3.0

0.40

brittle

21.2 19/59/22

8.5 81 None

40% HQ

›PET +

0.50 270/2.0

290/1.0

290/3.0

0.45

tough 19.6 21/64/25

14.9 79 209

40% HQ

›PET +

1.00 270/2.0

290/1.0

290/2.0

0.57

v. tough

17.1 22/65/13

11.2 85 None

40% HQ

›PET +

5.00 270/2.0

290/1.0

290/0.5(b)

0.24(c)

brittle

insol

insol 15.9 89 204

40% HQ

›PET +

5.00 270/2.0

290/1.0

290/0.8(b)

0.24(c)

brittle

insol

insol 27.9 87 204

40% HQ

__________________________________________________________________________

(a) Pressed films were lightmedium yellow.

(b) The melt viscosity was very high at the end of the polymerization.

__________________________________________________________________________

›PET MODIFIED WITH HYDROQUINONE AND ETHYLENE GLYCOL

Ethylene

Glycol Ester/

Catalyst

Used, Heat Heat Vacuum H Nmr

Mono/Bis

Starting

Sn/Ti Mole/Mole

Time Time Buildup

I.V.

Film HQ Ether of HQ Tg

Materials

ppm HQ °C./Hr.

°C./Hr.

dL/g

Strength

Mole %

%/%/%/ Mz/Mn

°C.

__________________________________________________________________________

›PET +

None/50

0.0 200-270/1.8

290/1.0

290/3.0

0.67

v. tough

15.6 23/66/11

8.9 85

40% HQ

›PET +

None/50

0.0 200-270/1.8

290/1.0

290/2.2

0.73

v. tough

13.1 28/62/10

9.8 84

40% HQ

›PET +

None/50

0.0 200-270/1.8

290/1.0

290/1.7

0.41

creasable

12.9 22/65/13

6.3 79

40% HQ

›PET +

None/50

0.1 270/1.0

290/1.0

290/1.7

0.59

tough

-- -- 7.1 80

40% HQ

›PET +

None/50

0.1 200-270/1.7

290/1.0

290/1.8

0.59

v. tough

17.8 16/70/14

8.3 80

40% HQ

›PET +

None/50

0.2 270/1.0

290/1.0

290/1.5

0.59

tough

-- -- 7.6 86

40% HQ

›PET +

None/50

0.2 200-270/1.8

290/1.0

290/1.8

0.55

v. tough

13.4 10/73/17

8.5 80

40% HQ

›PET +

None/50

0.5 200-270/2.2

290/1.0

290/1.9

0.75

v. tough

12.5 1/71/28

9.8 77

40% HQ

›PET +

None/50

0.5 270/1.3

290/1.0

290/3.0

0.42

tough

12.8 2/65/33

3.4 74

40% HQ (thin)

›PET +

150/None

0.5 200-270/2.2

290/1.0

290/2.9

0.56

v. tough

13.9 3/70/27

4.3 77

40% HQ

__________________________________________________________________________

›PET MODIFIED WITH PHENYLHYDROQUINONE

Vacuum

Catalyst

Heat Heat Buildup H Nmr

Starting

Sn/Ti,

Times

Temp/Time

I.V.

Film PHQ Tg Tm

Materials

ppm °C./Hr.

°C./Hr.

dL/g

Strength

Mole %

Mz/Mn

°C.

__________________________________________________________________________

PET + 40

None/50

270/1.0

290/1.0

290/3.0

0.35

brittle

17.6 3 78 None

›(PHQ)

PET + 40

None/150

270/3.0

290/1.0

290/2.3

0.36

brittle

23 2.9 85 None

›(PHQ)

PET + 40

600/None

270/3.0

290/1.0

290/0.8

0.41

brittle

insol

51.1 82 None

(PHQ) (a)

PET + 40

300/1500

270/3.0

290/1.2

290/2.8

0.62

creasable

26.9 18.5 89 None

›(PHQ)

__________________________________________________________________________

(a) Insoluble material noted in the I.V. solvent.

__________________________________________________________________________

›TEREPHTHALALTE POLYESTERS MODIFIED WITH HYDROQUINONE

Catalyst

Heat Heat Vacuum H Nmr

Starting

Sn/Ti,

Time Times Temp/Time

I.V.

Film HQ Tg Tm

Ex. Materials

ppm °C./Hr.

°C./Hr

°C./Hr.

dL/g

Strength

Mole %

Mz/Mn

°C.

__________________________________________________________________________

Polymer

Control

None -- -- -- 0.78

v. tough

-- -- 95 293

A (a)

79 A + 40(HQ)

None/100

270/1.0

280/1.0

290/0.17

0.57

v. tough

1.6 5.46 89 293

(a)

80 A + 40(HQ)

150/None

270/1.0

280/1.0

290/0.60

0.40

v. tough

3.9 2.61 89 293

(a)

Polymer

Control

None -- -- -- 0.79

v. tough

-- -- 85 261

B (b)

81 B + 40(HQ)

None/50

230/5.8

280/1.0

290/1.0

0.61

v. tough

1.3 3.3 88 262

(b) (d)

82 C + 40(HQ)

None/50

230/4.0

270/1.0

290/0.5

0.62

v. tough

10.3 4.7 84 None

(c)

__________________________________________________________________________

(a) Polymer A is poly(1,4cyclohexylenedimethylene terephthalate) prepared

with 40 ppm Ti catalyst, I.V. of 0.78 which had been dried at 110°

C. for 12 hours with full pump vacuum.

(b) Polymer B is poly(1,4cyclohexylenedimethylene terephthalate)

copolyester containing 17 mole % isophthalic acid prepared with 100 ppm T

catalyst, I.V. 0.79, which had been dried at 110° C. for 12 hours

with full pump vacuum.

mole % 1,4cyclohexanedimethanol prepared with 79 ppm Co, 44 ppm Mn, 52 pp

Ti, 8 ppm Sb, and 71 ppm P, I.V. 0.75, which had been dried at 110.degree

C. for 12 hours with full pump vacuum.

(d) Sample was heated at 230-270° C. for 5.8 hours.

__________________________________________________________________________

›MODIFICATION OF VARIOUS POLYESTERS WITH AROMATIC DIOLS

(a) Catalyst

Heat Heat Heat Vacuum H Nmr (b)

Starting

Sn/Ti

Times Times

Times

Buildup

I.V.

Film Diol Tg Tm

Ex.

Material

ppm °C./Hr.

°C./Hr.

dL/g

Strength

Mole %

Mz/Mn

°C.

__________________________________________________________________________

83 D + 30 (BPA)

150/0

230/4.0

250/1.0

270/1.0

290/2.1

1.09

brittle

14.2 41.9 73

None

84 F + 30 (HQ)

150/0

230/4.0

250/1.0

270/1.0

290/1.0

0.66

v. tough

7.1 25.1 80

None

85 G + 40 (HQ)

0/50

-- 270/1.0

290/1.0

290/2.7

0.41

brittle

19.0 8.5 119

231

86 G + 25 (HQ)

0/100

-- 270/1.0

290/1.0

300/4.0

0.75

tough 13.7 5.1 121

242

87 H + 30 (BPA)

150/0

230/4.0

240/1.0

250/1.0

250/2.52

0.49

v. tough

-- 8.8 41

211

88 I + 23 (BPA)

150/0

230/4.0

240/1.0

250/1.0

250/2.5

0.28

soft 16.3 3.4 -3 None

__________________________________________________________________________

(a) Polymer D is poly(ethylene isophthalate); Polymer F is poly(neopentyl

terephthalate); Polymer G is poly(ethylene 2,6napthalate); Polymer H is

poly(1,4butylene terephthalate); and Polymer I is poly(ethylene

succinate).

(b) Polymer D, poly(ethylene isophthalate), Tg 68° C.; Polymer F,

poly(neopentyl terephthalate), Tg 68° C.; Polymer G, poly(ethylene

2,6napthalate), Tg 125° C.; Polymer H, poly(1,4butylene

terephthalate), Tg 25° C.; and Polymer I, poly(ethylene succinate)

Tg -6° C.

Many variations will suggest themselves to those skilled in this art in light of the above detailed description. All such obvious modifications are within the full intended scope of the appended claims.

Claims

25 · 4 independent · depth 5

25 granted claims

›1.independentA poly(ester-ether) composition having improved thermal stability consisting essentially of repeat units from the reaction of (1) 10 to 175 mole perce…+13

›3.↳ 1The composition of claim 1 wherein the dihydroxy aromatic compound, component (1), is selected from the group consisting of hydroquinone, resorcinol, …d2+2

›6.↳ 1The composition of claim 1 wherein 20 to 60 mole percent, based on the repeat units of the polyester, of the dihydroxy aromatic compound is reacted wi…d2+1

›8.↳ 1The composition of claim 1 wherein the dicarboxylic acid, component (a) of the polyester, is selected from the group consisting of aliphatic dicarboxy…d2+3

›12.↳ 1The composition of claim 1 wherein the diol, component (b), of the polyester is selected from the group consisting of ethylene glycol, 1,3-butane diol…d2+1

›14.↳ 1The composition of claim 1 wherein the polyester, component (1), is polyethylene terephthalate.d2

›15.↳ 1A molded article comprising the composition of claim 1.d2

›2.independentA poly(ester-ether) composition having improved thermal stability consisting essentially of repeat units from the reaction of (1) 10 to 175 mole perce…+8

›24.independentA process for preparing a poly(ester-ether) having improved thermal stability consisting essentially of (I) reacting (1) 10 to 175 mole percent based …

›25.independentA process for preparing a poly(ester-ether) having improved thermal stability consisting essentially of (I) reacting (1) 10 to 175 mole percent based …

Classifications

19 codes

IPC · International Patent Classification

Section C — Chemistry; metallurgy

C08G63/672
C08G63/91

USPC · US Patent Classification

525/437528/298528/308.6528/97528/307528/102524/779264/176.1528/272528/308528/106524/783528/302528/283528/279528/88264/239

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Examiner

Samuel A. Acquah

art unit 153 · TC 1500

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